SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT
RULE 463 - ORGANIC
LIQUID STORAGE
(Adopted August 15, 1977)(Amended June 1, 1984)(Amended
December 7, 1990)
(Amended March 11, 1994)
(a)
Applicability
This rule applies to any above-ground stationary tank with a capacity of 75,000 liters (19,815 gallons) or greater used for storage of organic liquids, and any above-ground tank with a capacity between 950 liters (251 gallons) and 75,000 liters (19,815 gallons) used for storage of gasoline.
(b) Definitions
For purposes of this rule, the following definitions apply:
(A) Group I
chlorodifluoromethane (HCFC-22)
trifluoromethane (HFC-23)
dichlorotrifluoroethane (HCFC-123)
2-chloro-1,1,2,2-tetrafluoroethane
(HCFC-124)
pentafluoroethane (HFC-125)
1,1,2,2-tetrafluoroethane
(HFC-134)
tetrafluoroethane (HFC-134a)
dichlorofluoroethane
(HCFC-141b)
chlorodifluoroethane (HCFC-142b)
1,1,1-trifluoroethane
(HFC-143a)
1,1-diflouroethane (HFC-152a)
cyclic, branched, or linear,
completely fluorinated alkanes
cyclic, branched, or linear, completely
fluorinated ethers with no unsaturations
cyclic, branched, or linear,
completely fluorinated tertiary amines with no unsaturations
sulfur-containing perfluorocarbons with no unsaturations and with sulfur
bonds only to carbon and fluorine
(B) Group II
carbon tetrachloride
methylene chloride
1,1,1-trichloroethane
(methyl chloroform)
trichlorotrifluoroethane (CFC-113)
dichlorodifluoromethane (CFC-12)
trichlorofluoromethane (CFC-11)
dichlorotetrafluoroethane (CFC-114)
chloropentafluoroethane
(CFC-115)
Use of Group II compounds will be restricted in the future because they are either toxic or potentially toxic, or upper atmospheric ozone depleters, or cause other environmental impacts. Specifically, the District Board has established a policy to phase out chlorofluorocarbons (CFC), methyl chloroform (1,1,1-trichloroethane), and carbon tetrachloride on or before January 1, 1996.
(A) Category "A" seals are seals approved by the Executive Officer as most effective in the control of volatile organic compounds and are deemed Best Available Control Technology (BACT) according to the criteria set forth in Attachment A - "Floating Roof Tank Seal Categories."
(B) Category "B" seals are seals approved by the Executive Officer that are considered more effective than Category "C" seals based on the criteria set forth in Attachment A - "Floating Roof Tank Seal Categories."
(C) Category "C" seals are seals approved by the Executive Officer which are currently in service but are considered least effective in the control of volatile organic compounds.
(c) Tank Roof Requirements
No person shall place, store or hold in
any tank with a capacity of 150,000 liters (39,630 gallons) or greater, any
organic liquid having a true vapor pressure of 25.8 mm Hg (0.5 psi) absolute or
greater under actual storage conditions, and in any tank of more than 75,000
liters (19,815 gallons) capacity, any organic liquid having a true vapor
pressure of 77.5 mm Hg (1.5 psi) absolute or greater under actual storage
conditions, unless such tank is a pressure tank maintaining working pressures
sufficient at all times to prevent organic vapor loss to the atmosphere, or is
designed and equipped with one of the following vapor control devices, which is
properly installed and continuously maintained in good operating condition:
An external floating roof shall consist of a pontoon-type or double deck-type cover that continuously rests on the surface of the organic liquid and is equipped with a closure device between the tank shell and roof edge. The closure device shall consist of two seals, with one seal placed above the other. The seal below shall be designated as the primary seal, and the seal above shall be designated as the secondary seal. A seal which is not identified on the current list of seals approved by the Executive Officer shall not be installed or used unless the Executive Officer determines that such seal meets the applicable criteria of subparagraphs (c)(1)(A) through (c)(1)(C).
(A) A closure device on a welded or a riveted tank shell which uses a metallic shoe-type seal as its primary seal shall comply with the following requirements:
(i) Gaps between the tank shell and the primary seal shall not exceed 1.3 centimeters (1/2 inch) for a cumulative length of 30 percent of the circumference of the tank, and 0.32 centimeter (1/8 inch) for 60 percent of the circumference of the tank. No gap between the tank shell and the primary seal shall exceed 3.8 centimeters (1-1/2 inches). No continuous gap between the tank shell and the primary seal greater than 0.32 centimeter (1/8 inch) shall exceed 10 percent of the circumference of the tank.
(ii) Gaps between the tank shell and the secondary seal shall not exceed 0.32 centimeter (1/8 inch) for a cumulative length of 95 percent of the circumference of the tank. No gap between the tank shell and the secondary seal shall exceed 1.3 centimeters (1/2 inch).
(iii) Metallic shoe-type seals installed on or after August 1, 1977 shall be installed so that one end of the shoe extends into the stored organic liquid and the other end extends a minimum vertical distance of 61 centimeters (24 inches) above the stored organic liquid surface.
(iv) The geometry of the shoe shall be such that the maximum gap between the shoe and the tank shell is no greater than double the gap allowed by the seal gap criteria specified in clause (c)(1)(A)(i) for a length of at least 46 centimeters (18 inches) in the vertical plane above the liquid surface.
(B) A closure device which uses a resilient toroid-type seal as its primary seal shall comply with the applicable requirements of subparagraph (c)(1)(A).
(C) The primary and secondary seals shall comply with the following requirements:
(i) The primary seal envelope shall be made available for unobstructed inspection by the Executive Officer along its circumference. In the case of riveted tanks with resilient toroid-type seals, at least eight such locations shall be made available; for all other types of seals, at least four such locations shall be made available. If the Executive Officer deems it necessary, further unobstructed inspection of the primary seal may be required to determine the seal's condition along its entire circumference.
(ii) The secondary seal shall be installed in a way that permits the Executive Officer to insert probes up to 3.8 centimeters (1-1/2 inches) in width to measure gaps in the primary seal.
(iii) The secondary seal shall extend from the roof to the tank shell and shall not be attached to the primary seal.
(iv) Notwithstanding the secondary and the primary seal requirements of paragraph (c)(1), a secondary or primary seal may be loosened or removed for preventive maintenance, inspection or repair for a period not exceeding 72 hours with prior notification to the Executive Officer .
(D) All openings in the roof except pressure-vacuum valves, shall provide a projection below the liquid surface to prevent belching, escape, or entrainment of organic liquid, and shall be equipped with a cover, seal or lid. The cover, seal, or lid shall at all times be in a closed position, with no visible gaps, except when the device or appurtenance is in use. Pressure vacuum valves shall be set to within 10 percent of the maximum allowable working pressure of the roof.
(E) There shall be no holes, tears or openings in the secondary seal or in the primary seal envelope surrounding the annular vapor space enclosed by the roof edge, seal fabric, and secondary seal.
(F) Any emergency roof drain shall be provided with a slotted membrane fabric cover, or equivalent device, that covers at least nine-tenths (9/10) of the area of the opening.
A fixed roof tank equipped with an internal floating-type cover shall comply with the following requirements:
(A) A fixed roof tank with an existing internal floating-type cover approved by the Executive Officer on or before June 1, 1984, shall comply with the requirements applicable at the time such approval was given.
(B) A fixed roof tank which has an internal floating-type cover installed, modified, or replaced after June 1, 1984, shall have a closure device which consists of either a single liquid mounted primary seal or a primary and a secondary seal. All openings and fittings shall be fully gasketed or controlled in a manner specified by the Executive Officer. The closure device shall control vapor loss with an effectiveness equivalent to a closure device which meets the requirements of subparagraph (c)(1)(A). Seal designs not identified on the current list of seals approved by the Executive Officer shall not be installed or used unless the Executive Officer has given his prior written approval to its installation or use. For purposes of this paragraph, modification includes an identical replacement.
(C) The concentration of organic vapor in the vapor space above the internal floating-type cover shall not exceed 50 percent of its lower explosive limit (LEL) for those installed prior to June 1, 1984 and 30 percent of its LEL for those installed after June 1, 1984. Compliance shall be verified by the use of an explosimeter.
A fixed roof tank equipped with a vapor recovery system shall comply with the following requirements:
(A) Any tank gauging or sampling device on a tank vented to the vapor recovery system shall be equipped with a vapor-tight cover which shall be closed at all times except during gauging or sampling. The roof of such tank shall be properly maintained to be vapor tight with no holes, tears or uncovered openings.
(B) All piping, valves and fittings shall be constructed and maintained in a vapor-tight condition, in accordance with requirements of other District rules for such equipment.
(C) For purposes of this paragraph, the efficiency of a vapor recovery system shall be determined by making a comparison of controlled emissions to those emissions which would occur from a fixed cone roof tank holding the same organic liquid without a vapor control or vapor recovery system. The vapor recovery system shall have an efficiency of at least 95 percent by weight.
(d) Other Performance Requirements
(A) existing facilities for treatment of waste water used to refloat the tank roof; or
(B) facilities for equivalent emission control when refloating the roof with organic liquid.
(e) Self-Inspection of Floating Roof Tanks
Any owner or operator of a floating roof tank(s) shall conduct self-inspections of its tank(s) according to the following procedures:
(A) On or before September 14, 1994, each owner or operator shall submit an Inspection and Maintenance Plan to the Executive Officer for his/her approval. After September 14, 1994, each owner or operator constructing tank(s) subject to this rule shall submit an Inspection and Maintenance Plan, or a revision of its current Inspection and Maintenance Plan, to the Executive Officer prior to the completion of construction. The Inspection and Maintenance Plan shall include an inventory of tanks subject to this rule, the proposed self-inspection schedule, the number of certified persons to be dedicated to the program, any self-inspection procedures proposed in addition to those required by the District, and a copy of the owner or operator's safety procedures used for floating roof tanks. The tank inventory shall include tank identification number, maximum design capacity, product, shell type, dimensions, seal type and manufacturer, floating roof type, date of construction and location.
(A) All tanks subject to this rule shall be clearly and visibly identified by a sign on the outside wall for inventory, inspection and recordkeeping purposes.
(B) Any change(s) in tank identification shall require prior written approval by the Executive Officer.
(A) All tanks subject to this rule shall be inspected by a certified person twice per year at 4 to 8 months intervals according to the procedures and guidelines set forth in Attachment B - "Inspection Procedures and Compliance Report Form."
(B) The primary and secondary seals shall be inspected by a certified person each time a tank is emptied and degassed. Gap measurements shall be performed on an external floating roof tank when the liquid surface is still but not more than 24 hours after the tank roof is refloated.
(C) The Executive Officer shall be notified in writing at least 2 weeks prior to the start of any tank-emptying or roof-refloating operation for planned maintenance of a tank.
Any tank which does not comply with any provision of this rule shall be brought into compliance within 72 hours of the determination of non-compliance.
(A) All inspections shall be recorded on compliance inspection report forms approved by the Executive Officer as described in Attachment B - "Inspection Procedures and Compliance Report Form."
(B) All compliance inspection reports and documents shall be submitted to the Executive Officer within 5 working days of completion of the self-inspection.
(C) If a tank is determined to be in violation of the requirements of this rule, a written report shall be submitted to the Executive Officer within 120 hours of the determination of non-compliance, indicating corrective actions taken to achieve compliance.
(D) All records of owner or operator inspection and repair shall be maintained at the facility for a period of 3 years and shall be made available to the Executive Officer upon request.
(E) Emissions Reporting
(i) An owner or operator shall provide emissions information in a format consistent with Attachment C to the Executive Officer upon request. The requirement shall apply to all organic liquid storage tanks without regard to exemptions specified in subdivision (f).
(ii) An owner or operator shall provide all upset emissions information associated with product change, repair, and turnover or any other excess emission incidents.
(iii) An owner or operator shall maintain records of emissions data for all organic liquid storage tanks for the most recent two (2) year period.
(f) Exemptions
The provisions of this rule shall not apply to the following tanks, provided the person seeking the exemption supplies proof of the applicable criteria sufficient to satisfy the Executive Officer:
(A) The organic liquid contents fail to comply with paragraph (b) only when heated for shipment, and such heating occurs for not more than 48 hours and not more than once in any 20-day period; or
(B) The tank has a monthly average throughput of not more than 30 barrels of oil per day and was constructed prior to June 1, 1984.
(g) Test Methods
(A) vapor tight condition shall be determined at a distance of 1 cm. or less from the source ; and
(B) the soap bubble test shall not be used in lieu of quantitative test methods for vapor tightness determination.
SOUTH COAST AIR QUALITY MANAGEMENT DISTRICT
RULE 463 - ADDENDUM
Storage Temperatures Versus Actual Vapor Pressure
(Gravity/Initial Boiling Points Referenced)
|
Reference A - oAPI |
Temperature, oF |
Pressure | ||
|
Organic Liquids |
A |
B |
0.5 psia |
1.5 psia |
| Crude Oils | 12 | -- | -- | -- |
| 13 | -- | 120 | 180 | |
| 14 | -- | 85 | 145 | |
| 16 | -- | 60 | 107 | |
| 18 | -- | 55 | 93 | |
| 20 | -- | 52 | 84 | |
| 22 | -- | 49 | 77 | |
| 24 | -- | 45 | 73 | |
| 26 | -- | 42 | 70 | |
| 28 | -- | 40 | 67 | |
| 30 | -- | 38 | 64 | |
| Middle Distillates Kerosene Diesel Gas Oil Stove Oil 23 |
42.5 36.4 26.2 421 |
350 372 390 275 |
195 230 249 340 |
250 290 310 |
| Jet Fuels JP-1 JP-3 JP-4 JP-5 JP-7 |
43.1 54.7 51.5 39.6 44.50 |
330 110 150 355 360 |
165 -- 20 205 205 |
230 25 68 260 260 |
| Fuel Oil No. 1 No. 2 No. 3 No. 4 No. 5 No. 6 |
42.5 36.4 26.2 23 19.9 16.2 |
350 372 390 421 560 625 |
195 230 249 275 380 450 |
250 250 290 310 340 465 -- |
| Asphalts 60 - 100 pen. 120 - 150 pen. 200 -300 pen. |
-- -- -- |
-- -- -- |
490 450 360 |
550 500 420 |
| Acetone | 47.0 | 133 | -- | 35 |
| Acrylonitrile | 41.8 | 173 | 30 | 60 |
| Benzene | 27.7 | 176 | 35 | 70 |
| Carbon Disulfide | 10.6 (lb/gal) |
116 | -- | 10 |
| Carbon Tetrachloride | 13.4 | 170 | 30 | 60 |
| Chloroform | 12.5 (lb/gal) |
142 | -- | 40 |
| Cylohexane | 49.7 | 177 | 35 | 70 |
| 1,2 Dichloroethane (lb/gal) |
10.5 | 180 | 35 | 77 |
| Ethyl Acetate (lb/gal) |
23.6 | 171 | 35 | 70 |
| Ethyl Alcohol | 47.0 | 173 | 45 | 83 |
| Isopropyl Alcohol | 47.0 | 181 | 45 | 87 |
| Methyl Alcohol | 47.0 | 148 | -- | 50 |
| Methylene Chloride | 11.1 (lb/gal) |
104 | -- | 70 |
| Methylethyl Ketone | 44.3 | 175 | 30 | 70 |
| 1,1,1-Trichloroethane | 11.2 (lb/gal) |
165 | 60 | 100 |
| Trichloroethylene | 12.3 (lb/gal) |
188 | 50 | 91 |
| Toluene | 30.0 | 231 | 73 | 115 |
| Vinyl Acetate | 19.6 | 163 | -- | 60 |
ATTACHMENT A
FLOATING ROOF TANK SEAL CATEGORIES
PRIMARY SEALS
|
Category A |
Category B | Category C |
| 1. Liquid mounted multiple wipers with drip curtain and weight |
1. Liquid mounted single wiper with drip curtain and weight |
1. Liquid Mounted single wiper |
| 2. Liquid mounted mechanical shoe |
2. Liquid mounted double foam wipers with vapor curtain |
2. Liquid mounted foam log |
| 3. Vapor mounted primary wiper |
3. Liquid mounted foam log with vapor curtain | |
| 4. Vapor mounted E wiper |
4. Liquid mounted resilient toroid type liquid filled log | |
| 5. Vapor mounted double wipers |
5. Vapor mounted foam log/bag | |
| 6. Vapor mounted double foam wipers |
6. Vapor mounted foam wiper | |
| 7. Vapor mounted multiple wipers |
||
|
SECONDARY SEALS |
||
| 1. Multiple wipers | 1. Single wiper | 1. Liquid mounted wiper 2. Foam log/bag 3. Maloney |
Criteria used for categorization of floating roof tank seals:
ATTACHMENT B
INSPECTION PROCEDURES AND COMPLIANCE REPORT FORM
Equipment Needed:
Explosimeter (for internal floating roof tanks), liquid resistant measuring tape or device, tank probe (to measure gaps in tank seals - 1/8 inch, 1/2 inch, 1-1/2 inch), flashlight.
Inspection Procedures
o From the platform, conduct an overall visual inspection of the roof and check for obvious permit or rule violations. Record the information as shown under section F of the compliance report form.
o During visual inspection of the roof, check for unsealed roof legs, open hatches, open emergency roof drains or vacuum breakers and record the findings on the report accordingly. Indicate presence of any tears in the fabric of both seals.
o After the visual inspection, conduct an inspection of the entire secondary seal using the 1/8" and 1/2" probes. Record the gap data in section F(4) of the report.
o Conduct an inspection of the entire primary seal using the 1/8", 1/2", and 1 1/2" probes. Inspect the primary seal by holding back the secondary seal. Record the gap data in section F(5) of the report.
o Record all cumulative gaps between 1/8 inch and 1/2 inch ; between 1/2 inch and 1-1/2 inch ; and in excess of 1-1/2 inches, for both primary and secondary seals in section G of the report. Secondary seal gaps greater than 1/2 inch should be measured for length and width, and recorded in Comments under section (J) of the report.
o Using an explosimeter, measure the concentration of the vapor space above the internal floating roof in terms of lower explosive limit (LEL), and record the reading in section (E) of the report.
o Conduct a visual inspection of the roof openings and the secondary seal, if applicable, and record findings on the report.
RULE 463 COMPLIANCE REPORT The 4 page Rule 463 Compliance Report Form does not convert well. A copy of the form may be download as a part of the Rule 463.doc file.
ATTACHMENT C
DATA REPORTING REQUIREMENT FOR ROOF
TANKS
The data items shall include, but not be limited to, the
following:
| A. | External Floating Roof Tank | B. | Internal Floating Roof Tank | C. | Fixed Roof Tank |
|
|
|
|
|||
|
1. |
Tank I.D. |
1. |
Tank I.D. |
1. |
Tank I.D. |
|
2. |
Product Code |
2. |
Product Code |
2. |
Product Code |
|
3. |
Type of Floating Roof Seal |
3. |
Type of Floating Roof Seal |
3. |
Vent Type to Vapor Recovery System |
|
4. |
Shell Construction |
4. |
Shell Construction |
*4. |
Average Stock Storage Temperature |
|
5. |
Reid Vapor Pressure |
5. |
Reid Vapor Pressure |
5. |
True Vapor Pressure |
|
*6. |
Average Stock Storage Temperature |
*6. |
Average Stock Storage Temperature |
6. |
Tank Diameter |
|
7. |
True Vapor pressure |
7. |
True Vapor Pressure |
*7. |
Vapor Molecular Weight |
|
8. |
Tank Diameter |
8. |
Tank Diameter |
8. |
Average Outage |
|
*9. |
Wind Speed Exponent |
*9. |
Wind Speed Exponent |
*9. |
Average Daily Temperature Change |
|
*10. |
Average Wind Velocity |
*10. |
Average Wind Velocity |
10. |
Throughput |
|
*11. |
Seal Factor |
*11. |
Seal Factor |
11. |
Turnover Factor |
|
*12. |
Product Factor |
*12. |
Product Factor |
*12. |
Turnovers Per Year |
|
*13. |
Vapor Molecular Weight |
*13. |
Vapor Molecular Weight |
*13. |
Adjustment Factor for Small Tank |
|
*14. |
Clingage Factor |
*14. |
Clingage Factor |
*14. |
Paint Factor |
|
15. |
Throughput |
15. |
Throughput |
*15. |
Crude-Oil Factor (Breathing) |
|
*16. |
Density of Liquid Stock |
*16. |
Density of Liquid Stock |
*16. |
Crude-Oil Factor (Working) |
|
17. |
Total Number of Different Type of Fitting |
*17. |
Number of Columns |
17. |
Breathing Loss |
|
18. |
Total Roof Fitting Loss Factor |
*18. |
Effective Column Diameter |
18. |
Working Loss |
|
19. |
Vapor Pressure Function |
19. |
Total Number of Different Types of Fittings |
19. |
Total Loss (Without Vapor Recovery) |
|
20. |
Roof Fitting Loss |
*20. |
Total Deck Fitting Loss Factor |
*20. |
Vapor Recovery System Efficiency |
|
21. |
Standing Loss |
21. |
Vapor Pressure Function |
21. |
Total Loss (With Vapor Recovery) |
|
22. |
Withdrawal Loss |
*22. |
Deck Seam Length Factor |
22. |
Number of Excess Upset Emissions Incidents |
|
23. |
Total Loss |
*23. |
Deck Seam Loss per Unit |
23. |
Total Excess Upset Emissions |
|
24 |
Number of Excess Upset Emissions Incidents |
24. |
Deck Seam Loss |
|
|
|
25. |
Total excess Upset Emissions |
25. |
Deck Fitting Loss |
|
|
|
|
26. |
Standing Loss |
|
||
|
|
27. |
Withdrawal Loss |
|
||
|
|
28. |
Total Loss |
|
||
|
|
29. |
Number of Excess Upset Emissions Incidents |
|
||
|
|
30. |
Total Excess Upset Emissions |
|
* Default values are available from the District
The Data format and order shall be specified and approved by the Executive Officer.
Appendix A
SAMPLE ORGANIC LIQUID STORAGE TANKS
ANNUAL
EMISSIONS SAMPLE DATA REPORTING REQUIREMENTS
External Floating Roof
Tank
|
|
A |
B |
C |
D |
E |
F |
G |
H |
I |
J |
K |
L |
|
1 |
TANK I.D. |
PRODUCT CODE |
TYPE OF FLOATING ROOF SEAL |
SHELL CONSTRUCTION |
REID VAPOR PRESSURE |
AVE. STOCK STOR. EMP. |
TRUE VAPOR PRESSURE |
TANK DIAMETER |
WIND SPEED EXP. |
AVE. WIND VELOCITY |
SEAL FACTOR |
PRODUCT FACTOR |
|
2 |
|
|
|
|
psi |
F |
psia |
feet |
|
mile/hour |
|
|
|
3 |
1 |
6 |
1C |
W |
2 |
68 |
1.1 |
80 |
1 |
6.8 |
0.2 |
0.4 |
|
4 |
2 |
3 |
1C |
W |
0.03 |
68 |
0.01 |
95.5 |
1 |
6.8 |
0.2 |
1 |
|
5 |
3 |
9 |
1C |
W |
0 |
68 |
0 |
95.5 |
1 |
6.8 |
0.2 |
1 |
|
6 |
4 |
3 |
1C |
W |
0.03 |
68 |
0.01 |
90 |
1 |
6.8 |
0.2 |
1 |
|
7 |
25 |
5 |
4A |
R |
0.2 |
68 |
0.01 |
117.2 |
1.5 |
6.8 |
1.3 |
1 |
|
8 |
26 |
5 |
1A |
W |
0.2 |
68 |
0.01 |
120 |
1.5 |
6.8 |
1.2 |
1 |
|
9 |
27 |
9 |
1A |
W |
0 |
99 |
0 |
120 |
1.5 |
6.8 |
1.2 |
1 |
|
|
M |
N |
O |
P |
Q |
R |
S |
T |
U |
V |
|
1 |
VAPOR |
CLINGAGE |
THROUGHPUT |
DEN. OF LIQUID |
TOTAL NO. OF |
TOTAL ROOF |
VAPOR |
ROOF FITTING |
STANDING |
WITHDRAWAL |
|
2 |
lb/lb Mole |
bbl/1000 sq. ft. |
bbl/year |
lb/gal |
|
lb mole/year |
|
lbs/year |
lbs/year |
lbs/year |
|
3 |
50 |
0.6 |
334914 |
7.1 |
3 |
147.3 |
2 |
55 |
42 |
168 |
|
4 |
130 |
0.15 |
234841 |
7.1 |
3 |
152.3 |
0 |
3 |
3 |
25 |
|
5 |
190 |
0.15 |
73651 |
7.9 |
3 |
152.3 |
0 |
0 |
0 |
9 |
|
6 |
130 |
0.15 |
151702 |
7.1 |
3 |
146.6 |
0 |
3 |
2 |
17 |
|
7 |
130 |
0.15 |
184615 |
7 |
3 |
158.6 |
0 |
3 |
60 |
16 |
|
8 |
130 |
0.15 |
2223784 |
7 |
3 |
162.1 |
0 |
3 |
19 |
183 |
|
9 |
190 |
0.15 |
773173 |
7.9 |
2 |
162.1 |
0 |
0 |
0 |
72 |
|
|
W |
X |
Y |
|
1 |
TOTAL LOSS |
NO. OF |
TOTAL UPSET |
|
2 |
lbs/year |
|
lb/year |
|
3 |
265 |
0 |
0 |
|
4 |
30 |
2 |
0.1 |
|
5 |
9 |
0 |
0 |
|
6 |
22 |
0 |
0 |
|
7 |
79 |
0 |
0 |
|
8 |
206 |
0 |
0 |
|
9 |
73 |
0 |
0 |
Appendix B
SAMPLE ORGANIC LIQUID STORAGE TANKS
ANNUAL EMISSIONS
SAMPLE DATA REPORTING REQUIREMENTS
Internal Floating Roof Tank
|
|
A |
B |
C |
D |
E |
F |
G |
H |
I |
J |
K |
L |
|
1 |
TANK I.D. |
PRODUCT CODE |
TYPE OF FLOATING ROOF SEAL |
SHELL CONSTRUCTION |
REID VAPOR PRESSURE |
AVE. STOCK STOR. EMP. |
TRUE VAPOR PRESSURE |
TANK DIAMETER |
WIND SPEED EXP. |
AVE. WIND VELOCITY |
SEAL FACTOR |
PRODUCT FACTOR |
|
2 |
|
|
|
|
psi |
F |
psia |
feet |
|
mile/hour |
|
|
|
3 |
12 |
2 |
5A |
W |
3.4 |
140 |
6.2 |
64 |
0 |
6.8 |
3 |
0.4 |
|
4 |
13 |
2 |
6A |
W |
3.4 |
140 |
6.2 |
64 |
0 |
6.8 |
6.7 |
0.4 |
|
|
M |
N |
O |
P |
Q |
R |
S |
T |
U |
V |
|
1 |
VAPOR |
CLINGAGE |
THROUGHPUT |
DEN. OF LIQUID |
NO. OF |
EFFECTIVE |
TOTAL NO. OF |
TOTAL DECK |
VAPOR |
DECK SEAM LEN. |
|
2 |
lb/lb Mole |
bbl/1000 sq. ft. |
bbl/year |
lb/gal |
|
feet |
|
lb mole/year |
|
1/ft |
|
3 |
50 |
0.006 |
466095 |
7.1 |
1 |
1 |
0 |
105 |
0.14 |
0 |
|
4 |
50 |
0.006 |
466095 |
7.1 |
1 |
1 |
0 |
210 |
0.14 |
0 |
|
|
W |
X |
Y |
Z |
AA |
AB |
AC |
AD |
|
1 |
DECK SEAM |
DECK SEAM LOSS |
DECK |
STANDING |
WITHDRAWAL |
TOTAL LOSS |
NO. OF |
TOTAL UPSET |
|
2 |
lb mole/ft year |
lbs/year |
lbs/year |
lbs/year |
lbs/year |
lbs/year |
|
lbs/year |
|
3 |
0 |
0 |
286 |
523 |
297 |
1106 |
0 |
0 |
|
4 |
0 |
0 |
571 |
1167 |
297 |
2035 |
0 |
0 |
Appendix C
SAMPLE ORGANIC LIQUID STORAGE TANKS
ANNUAL EMISSIONS
SAMPLE DATA REPORTING REQUIREMENTS
Fixed Roof Tank
|
|
A |
B |
C |
D |
E |
F |
G |
H |
I |
J |
K |
|
1 |
TANK I.D. |
PRODUCT CODE |
VENT TYPE TO |
AVE. STOCK |
TRUE VAPOR |
TANK |
VAPOR |
AVE. |
AVE. DAILY |
THROUGHPUT |
TURNOVER |
|
2 |
|
|
|
|
psi |
F |
psia |
feet |
F |
bbl/year |
|
|
3 |
210 |
9 |
N |
99.99 |
0 |
120 |
190 |
14 |
16 |
300027 |
1 |
|
4 |
285 |
9 |
N |
99.99 |
0 |
35 |
190 |
0 |
16 |
151414 |
1 |
|
5 |
286 |
9 |
N |
99.99 |
0 |
35 |
190 |
0 |
16 |
151414 |
1 |
|
6 |
294 |
9 |
V |
68 |
0 |
120 |
190 |
20 |
16 |
505615 |
1 |
|
|
L |
M |
N |
O |
P |
Q |
R |
S |
T |
|
1 |
TURNOVERS PER YEAR |
ADJ. FACTOR FOR |
PAINT FACTOR |
CRUDE OIL FACTOR |
CRUDE OIL |
BREATHING |
WORKING LOSS |
TOTAL LOSS |
VAPOR RECOVERY |
|
2 |
|
|
|
|
|
lbs/year |
lbs/year |
lbs/year |
|
|
3 |
4 |
1 |
1 |
1 |
1 |
56 |
3 |
60 |
0 |
|
4 |
30 |
1 |
1 |
1 |
1 |
0 |
2 |
2 |
0 |
|
5 |
30 |
1 |
1 |
1 |
1 |
0 |
2 |
2 |
0 |
|
6 |
6 |
1 |
1 |
1 |
1 |
68 |
6 |
74 |
95 |
|
|
U |
V |
W |
|
1 |
TOTAL LOSS (w/ |
NO. OF EXCESS |
TOTAL UPSET |
|
2 |
lbs/year |
|
lb/year |
|
3 |
60 |
0 |
0 |
|
4 |
2 |
0 |
0 |
|
5 |
2 |
0 |
0 |
|
6 |
4 |
0 |
0 |